CN1171927C - Method for production of polyether alcohols - Google Patents
Method for production of polyether alcohols Download PDFInfo
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- CN1171927C CN1171927C CNB008170738A CN00817073A CN1171927C CN 1171927 C CN1171927 C CN 1171927C CN B008170738 A CNB008170738 A CN B008170738A CN 00817073 A CN00817073 A CN 00817073A CN 1171927 C CN1171927 C CN 1171927C
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/04—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers only
- C08G65/06—Cyclic ethers having no atoms other than carbon and hydrogen outside the ring
- C08G65/08—Saturated oxiranes
- C08G65/10—Saturated oxiranes characterised by the catalysts used
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/26—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
- C08G65/2642—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds characterised by the catalyst used
- C08G65/2645—Metals or compounds thereof, e.g. salts
- C08G65/2663—Metal cyanide catalysts, i.e. DMC's
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4833—Polyethers containing oxyethylene units
- C08G18/4837—Polyethers containing oxyethylene units and other oxyalkylene units
- C08G18/485—Polyethers containing oxyethylene units and other oxyalkylene units containing mixed oxyethylene-oxypropylene or oxyethylene-higher oxyalkylene end groups
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
- C08G65/26—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
- C08G65/2696—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds characterised by the process or apparatus used
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- Organic Chemistry (AREA)
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- Polyurethanes Or Polyureas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
The invention relates to a method for the production of polyether alcohols by catalytic addition of at least two alkylene oxides to H-functional starting materials. Said method is characterised in that at least one multi-metal cyanide compound is used as catalyst and in the course of the addition to the starting material at least one oxyalykylene unit is incorporated, during which a common dosing of at least two alkylene oxides occurs, whereby during said common dosing the ratio of the amounts of alkylene oxides to each other is varied.
Description
The purposes that the present invention relates to Aethoxy Sklerol, its preparation method and be used to produce urethane.
Aethoxy Sklerol is used to produce urethane in a large number.Rudimentary oxyalkylene, particularly oxyethane and propylene oxide catalysis are added on the H-functional initiator material prepare Aethoxy Sklerol.As catalyzer, use alkali metal hydroxide or salt usually, wherein potassium hydroxide has most important industrial significance.
Many industrial application are used Aethoxy Sklerol, and its polyether chain is by forming more than a kind of oxyalkylene.In industry, use rudimentary oxyalkylene usually, for example oxyethane, propylene oxide and butylene oxide ring, wherein oxyethane and propylene oxide have most important industrial significance.The molecule addition is undertaken by the block method, for example only a kind of oxyalkylene of an addition.The Aethoxy Sklerol that makes thus has such polyether chain, and wherein a kind of oxyalkylene segment is arranged in order.The another kind of possible method for preparing Aethoxy Sklerol from least two kinds of oxyalkylenes is the atactic molecule addition (being called assorted molecule addition) of oxyalkylene.Wherein, the form of oxyalkylene with mixture is metered in the reaction mixture.These mixtures contain the oxyalkylene of mutual proportions constant usually.The method of this introducing oxyalkylene is called " tradition is random " hereinafter.Ratio used herein is the ratio of each oxyalkylene amount, and wherein " amount " is that weight or its molar weight of expression oxyalkylene are not important, for example represented by unit " mole ".
When use had high catalytic activity catalyst, the known preparation method's of Aethoxy Sklerol shortcoming was remarkable especially, caused the molecule addition of oxyalkylene to be carried out under two-forty.So, when multi-metal cyanide catalyzer (being also referred to as dmc catalyst) was used for molecule addition by multiple oxyalkylene and prepares Aethoxy Sklerol, many quality problems about Aethoxy Sklerol usually appearred.The molecule addition of the oxyalkylene that carries out with block fashion causes the very wide molecular weight distribution and the muddiness of Aethoxy Sklerol usually, and the content that random method causes link ends oxyethane segment usually is for many occasions and Yan Taigao.Oxyethane end segment adds on the block of random mixture of propoxylated glycerine or oxyalkylene and causes forming very high-molecular weight ethoxylate, and it has fettered the most of oxyethane that is added.For processing, the viscosity of these polyvalent alcohols is too high.Another consequence of this situation is in order to reach the high-content of the required end ring oxidative ethane of active polyvalent alcohol, and the ethylene oxide content in the Aethoxy Sklerol must be very high, causes the wetting ability of polyethers to increase greatly.Even can obtain under the situation of polyurethane foamed material by processing these polyethers, this also causes forming the foam materials that is easy to very much hydrolysis.Another problem normally owing to as the various organic or inorganic materials of common prescription component in the polyurethane production for example water, glycerine and catalyzer must be dissolved in the production process of polyol component that polyvalent alcohol causes, wherein said polyol component is used for urethane reaction subsequently.So the type of block, block length and block distributed are subjected to strict restriction usually.
WO97/27236 (EP 876416) discloses a kind of Aethoxy Sklerol that is used for the high elasticity soft foam materials, this Aethoxy Sklerol comprises the interior block that contains the propylene oxide that is no more than oxyalkylene total amount 35 weight % and one or morely has ethylene oxide content and be at least the oxyethane of 2 weight % and the outer block of propylene oxide, part is by catalysis at least for block in wherein being somebody's turn to do, and outer block is by the complete catalysis of multi-metal cyanide catalyzer.But this Aethoxy Sklerol Aethoxy Sklerol than commercially available base catalysis usually is much more active, so can not introduce in the known polyurethane system.In addition, Aethoxy Sklerol obtained by this method is normally muddy.
The problems referred to above are obvious especially under the situation of polyurethane foamed material, particularly flexible foams, and are the most remarkable under the situation of soft offset plate (slabstock) foam materials.Particularly, this foam materials forms crackle, and the decline of mechanical property occurs.
When using the multi-metal cyanide catalyzer, can only under the situation of sacrificing high-hydrophilic and very high viscosity, obtain high-load primary hydroxyl end group by oxyethane end block.
DD-A-275 695 discloses a kind of method for preparing Aethoxy Sklerol, and wherein oxyethane and propylene oxide are with the form addition of random mixture, and wherein the ratio of each oxyalkylene raises equably or reduces.But, because low as the catalytic activity of the potassium hydroxide of catalyzer, so the introducing ratio of oxyalkylene in polyether chain is not identical with its reinforced ratio, but by with introduce in advance, also the oxyalkylene of addition does not carry out back mixing and changes.So required block structure can only reach limited degree, and the performance of the Aethoxy Sklerol that makes with the random method of tradition sometimes of the performance of the Aethoxy Sklerol that makes thus is almost as broad as long.Although this defective can be added by metering slowly and be alleviated, this will cause uneconomic long pause time.Use for example potassium hydroxide of active not too high catalyzer, cause unwanted side reaction in synthetic, this causes the loss and the infringement quality product of oxyalkylene.So, can not be less than 0.4 iodine number, still there is the side reaction of certain degree in this expression.The formation of unsaturated component causes the loss of hydroxy functional group especially, makes that required Aethoxy Sklerol amount increases in polyurethane reaction.In addition, formation coloured or by product odorous influences the quality of the Aethoxy Sklerol that makes thus unfriendly.
In addition, starting point and the terminal point of introducing in the metering of oxyalkylene described in the DD-A-275695 must all be pure zirconia alkene in each case.So the random block described in the DD-A-275695 can not always advantageously make up with traditional random block.Therefore, can not obtain having the polyvalent alcohol of moderate content primary hydroxyl.In addition, always contain the segment of forming by pure ethylene oxide by this method from the Aethoxy Sklerol that oxyethane prepares.The muddiness that this causes unwanted height facile hydrolysis, high viscosity and is easy to occur polyethers.If these atactic polyethers are with ethylene oxide-capped, then the back mixing effect is excessive, causes some propylene oxide always to appear at link ends.
An object of the present invention is to provide and to add to the Aethoxy Sklerol for preparing on the H-functional initiator material by at least two kinds of oxyalkylene catalysis, this Aethoxy Sklerol is haze-free, have the viscosity of being convenient to process, and can process without a doubt and obtain urethane, particularly flexible polyurethane foams.In addition, should be able to regulate according to the target mode at the content of the oxyalkylene of polyether chain end.Should avoid occurring the high molecular last-of-chain, this phenomenon can occur in the molecule addition at oxyalkylene when preparing Aethoxy Sklerol by traditional block method with dmc catalyst.In addition, should avoid generally necessary long-term conversion and pressure-stabilisation stage between each block.
We find, this purpose can realize by a kind of method for preparing Aethoxy Sklerol, at least two kinds of oxyalkylene catalysis are added on the H-functional initiator material, wherein in the process that oxyalkylene catalysis is added on the initiator material, at least once unite and introduce two kinds of oxyalkylenes, and in the introducing process, change the ratio of each oxyalkylene in this mixture.
This form that is metered into oxyalkylene will be called dynamic approach hereinafter.
In order to realize purpose of the present invention, term " ratio " refers to the ratio of each oxyalkylene amount of being metered in dynamic approach.
Therefore the present invention provides a kind of method for preparing Aethoxy Sklerol on the H-functional initiator material that adds to by at least two kinds of oxyalkylene catalysis, wherein at least a multimetal cyanide compounds is as catalyzer, and the addition of oxyalkylene on the initiator material comprises introduces at least a oxyalkylene block, in forming this block process, at least two kinds of oxyalkylenes are metered into together, and change the ratio between each oxyalkylene in this metering mixture in uniting the introducing process.
The purposes that the present invention also provides the Aethoxy Sklerol that makes by described method and is used to produce urethane, particularly flexibel polyurethane, and relate to the urethane that uses this Aethoxy Sklerol to make.
The variation of oxyalkylene ratio can be linear or nonlinear.The linear change of oxyalkylene ratio refer to the oxyalkylene ratio in any equal timed interval with identical quantitative changeization.In this case, the time dependent relation curve of oxyalkylene ratio is a straight line.The nonlinearities change of oxyalkylene ratio refer to this ratio in the timed interval that equates with different quantitative changeizations.In this case, the time dependent relation curve of oxyalkylene ratio is not a straight line.This curve can be an index curve.
Can design dynamic approach like this, make that the oxyalkylene total amount that is metered into is a constant in given interval, but the oxyalkylene total amount that is metered into also may change in whole dynamic approach in given interval in whole dynamic approach.This amount that is can be by the amount that keeps a kind of oxyalkylene constant and that change another kind of oxyalkylene realizes, maybe can realize by the amount that changes two kinds of oxyalkylenes.Under latter event, the ratio between the various oxyalkylenes must change as mentioned above.
Dynamic approach can be carried out by this way, i.e. a kind of content of oxyalkylene continuous decrease in this process wherein, and the aequum of this oxyalkylene in reaching this mixture, or only continue to add another kind of oxyalkylene.Dynamic approach also can be carried out by this way, and promptly a kind of content of oxyalkylene continues to increase earlier in this mixture, reduces immediately then or continuous decrease after the constant ratio stage of oxyalkylene.When dynamic approach begins and finish, wherein in each case, can there be a kind of oxyalkylene or this two kinds of oxyalkylenes in the incoming mixture.
In the simplest embodiment of the inventive method, whole polyether chain is made of the single block by the dynamic approach addition.
But, preferably add on only a part of polyether chain, and add on the remaining oxyalkylene by known block or random method by dynamic approach.Herein, can introduce in the polyether chain by one or more oxyalkylene blocks of dynamic approach addition.
Head, afterbody or the centre of polyether chain can be positioned at by the oxyalkylene block of dynamic approach addition.
When the dynamic approach addition oxyalkylene block, can be to this block with at least one block direct addition that forms by a kind of oxyalkylene only.This preferably forms in the incoming mixture subsequently by reducing continuously to be not used in that the content of the oxyalkylene of block carries out in dynamic approach, finally be 0 until the content of this oxyalkylene in this mixture, only continues to be metered into another kind of oxyalkylene then.But, when dynamic approach finishes, in this mixture, also may still there be two kinds of oxyalkylenes, and also may introduce wherein a kind of oxyalkylene, stop then adding, continuous measurement adds another kind of oxyalkylene simultaneously.
At least one block that contains two kinds of oxyalkylenes also can be by traditional random method direct addition to passing through on the oxyalkylene block of dynamic approach addition.Herein, can carry out dynamic approach, be that subsequently random block carries out addition with this ratio until the ratio of each oxyalkylene, continues then to introduce oxyalkylene with this ratio, maybe can stop dynamic measurement and add, then continuously will add to the ratio continuous measurement adding oxyalkylene on the block subsequently.
Also can be by at least one block by only a kind of oxyalkylene of traditional random fashion addition or two kinds of oxyalkylenes before the dynamic approach addition oxyalkylene block.Herein, can be identical or different at the oxyalkylene ratio of this tradition block end with the oxyalkylene ratio when dynamic approach begins.
As mentioned above, can with dynamical fashion with this block direct addition to the initiator material, this block can be as mentioned above contain one or both oxyalkylenes when beginning is introduced in metering, and can be metered into by above-mentioned several modes of dynamic approach.As mentioned above, after this can be by traditional random method addition at least a pure zirconia alkene block or at least a oxyalkylene block.This polyether chain can also comprise at least a another kind of oxyalkylene block that passes through the dynamic approach addition.
In addition, can also introduce in link ends by the oxyalkylene block of dynamic approach addition.Under the situation of this block, the above-mentioned embodiment of all of dynamic approach also is possible.Therefore, this block can contain one or both oxyalkylenes when beginning, can be metered into this one or both oxyalkylenes then when being metered into end.
By random method addition and be positioned under the situation of polyether chain intermediary oxyalkylene block, also can similarly adopt all above-mentioned embodiments.They therefore can be in abutting connection with the oxyalkylene block that only contains a kind of oxyalkylene or traditional random block, it forms with the composition of this block when dynamic approach begins identical or different, the oxyalkylene that these blocks only contain the oxyalkylene that is metered into separately in advance or are metered into the form of mixtures of the oxyalkylene that is used to introduce dynamic block when beginning is added in metering.Similarly, only one or both oxyalkylenes may reside in the end of dynamic block.Then, similarly addition pure zirconia alkene block or traditional random oxyalkylene block, wherein the oxyalkylene ratio of this block head can be identical or different with the oxyalkylene ratio of dynamic block afterbody.
The traditional Aethoxy Sklerol that is used to produce soft molded polyurethane foam material or polyurethane elastomer has interior block usually, and it contains propylene oxide or contains oxyethane and traditional random mixture of propylene oxide.This comes adjacency by the pure ethylene oxide block, and it is necessary that this block provides the high-content primary hydroxyl.When using the multi-metal cyanide catalyzer, this method obtains highly viscous, muddy polyethers, and its proportion of primary OH groups is low.Although can improve proportion of primary OH groups by the molecule addition of longer ethylene oxide chain, this also causes the wetting ability increasing degree of Aethoxy Sklerol excessive.But, if the block that when metering add to finish ethylene oxide content is improved adds to end by traditional random block or the polyether chain only made by a kind of oxyalkylene block by dynamic approach, and need just can not obtain the primary hydroxyl of desired content at the long block of link ends addition of ethylene oxide.
By contrast, when polyvalent alcohol is used for soft offset plate foam materials, preferably use proportion of primary OH groups less than 10% Aethoxy Sklerol.On the other hand, should have the oxyethane of certain content in chain, because the oxyethane in polyether chain has improved water and the various solubleness of additive in polyvalent alcohol required in polyurethane production, in addition, oxyethane is also cheap than propylene oxide.In addition, the certain content oxyethane in outside polyether chain is useful for avoiding obtaining closed-cell foam material.But in the random method of tradition, ethylene oxide content can not surpass specific limit, and this is because the polyepoxyethane of crossing of link ends causes proportion of primary OH groups to increase undesirably.But, if by dynamic approach addition oxyalkylene intermixture, wherein by the ethylene oxide content that is reduced in the oxyalkylene intermixture this content is reduced towards the chain extreme direction, then high-load oxyethane can be introduced in the chain, and can not cause because primary hydroxyl makes the active detrimental action that increases.Other the short block that occurs pure propylene oxide in link ends also is possible.
The inventive method is particularly advantageously carried out with the multi-metal cyanide catalyzer, because this catalyzer has very high activity, is introduced in the chain immediately so guarantee the oxyalkylene that is added.
These catalyzer have formula (I) structure usually
M
1 a[M
2(CN)
b(A)
c]
d·fM
1gX
n·h(H
2O)·eL (I)
Wherein
M
1Be metal ion, be selected from Zn2+, Fe2+, Co3+, Ni2+, Mn2+, Co2+, Sn2+, Pb2+, Mo4+, Mo6+, Al3+, V4+, V5+, Sr2+, W4+, W6+, Cr2+, Cr3+, Cd2+,
M
2Be metal ion, be selected from Fe2+, Fe3+, Co2+, Co3+, Mn2+, Mn3+, V4+, V5+, Cr2+, Cr3+, Rh3+, Ru2+, Ir3+,
And M
1And M
2Can be identical or different,
A is a negatively charged ion, is selected from halogen ion, hydroxide radical, sulfate radical, carbonate, prussiate, thiocyanate radical, isocyano, cyanate radical, carboxylate radical, oxalate and nitrate radical,
X is a negatively charged ion, is selected from halogen ion, hydroxide radical, sulfate radical, carbonate, prussiate, thiocyanate radical, isocyano, cyanate radical, carboxylate radical, oxalate and nitrate radical,
L is the water miscibility part, is selected from alcohol, aldehyde, ketone, ether, polyethers, ester, urea, acid amides, nitrile and thioether,
With
Select a, b, c, d, g and n make this compound be electric neutrality and
E is the ligancy of part, is mark or integer more than or equal to 0,
F be more than or equal to 0 mark or integer and
H is mark or the integer more than or equal to 0.
These compounds prepare by known method, wherein make aqueous solution, particularly salt or the acid of the aqueous solution and the six cyano group metallides of water-soluble metal salt, and in mixing solutions or add water soluble ligand afterwards.
The common consumption of catalyzer is less than 1 weight %, preferably less than 0.5 weight %, especially preferably less than 1000ppm, especially less than 500ppm, in each case all in the weight of Aethoxy Sklerol.
The oxyalkylene that is used for the inventive method is an oxyethane, 1,2-epoxy group(ing) propane (propylene oxide), 1,2-methyl-2-ethyl propyl ether, 1,2-epoxy group(ing) butane, 2,3-epoxy group(ing) butane (butylene oxide ring), 1,2-methyl-3-ethoxy butane, 1,2-epoxy group(ing) pentane, 1,2-methyl-3-ethoxy pentane, 1,2-epoxy group(ing) hexane, 1,2-epoxy group(ing) heptane, 1,2-epoxy group(ing) octane, 1,2-epoxy group(ing) nonane, 1,2-epoxy group(ing) decane, 1,2-epoxy group(ing) undecane, 1,2-epoxy group(ing) dodecane, Styrene oxide 98min., 1,2-epoxy group(ing) pentamethylene, 1, the 2-epoxy-cyclohexane, (2, the 3-epoxypropyl) benzene, vinyl oxyethane, 3-phenoxy group-1,2-epoxy group(ing) propane, 2,3-epoxy group(ing) (methyl ether), 2,3-epoxy group(ing) (ethyl ether), 2,3-epoxy group(ing) (isopropyl ether), 2,3-epoxy group(ing)-1-propyl alcohol, stearic acid 3,4-epoxy group(ing) butyl ester, acetate 4,5-epoxy group(ing) pentyl ester, methacrylic acid 2,3-epoxy group(ing) propyl ester, vinylformic acid 2,3-epoxy group(ing) propyl ester, Glycidyl butyrate, the glycidic acid methyl ester, 2,3-epoxy group(ing) ethyl butyrate, 4-(trimethyl silyl) butane 1, the 2-epoxide, 4-(triethylsilyl) butane 1, the 2-epoxide, 3-(perfluoro-methyl) propylene oxide, 3-(perfluor ethyl) propylene oxide, 3-(perfluoro butyl) propylene oxide, 4-(2, the 3-epoxypropyl) morpholine or 1-(oxyethane-2-ylmethyl) pyrrolidin-2-one.
Preferred oxyethane, propylene oxide and the butylene oxide ring of using, special optimization ethylene oxide and propylene oxide
Used H-functional initiator material is 2-to 8-functional alcohol particularly.In order particularly advantageously to prepare the Aethoxy Sklerol that is used for flexible polyurethane foams by the inventive method, useful especially initiator material is difunctionality and trifunctional alcohol, for example ethylene glycol, glycol ether, triglycol, propylene glycol, dipropylene glycol, 3 third glycol, glycerine, TriMethylolPropane(TMP) or tetramethylolmethane.Described alcohol can use separately or use with the form of mixture.
In order to carry out the inventive method, when beginning to react, the initiator material is placed reactor, in case of necessity, can remove and anhydrate and other volatile compound.This is undertaken by distillation usually, preferably under reduced pressure or under vacuum carries out with the vector gas stripping.Catalyzer may reside in the initiator material, but also can only add catalyzer after pre-treatment initiator material.Under latter event, catalyzer stands less thermal stresses.Before adding oxyalkylene, make reactor be inertia usually, to avoid the unwanted reaction of oxyalkylene and oxygen.Be metered into oxyalkylene then, wherein the molecule addition is carried out in the above described manner.The molecule addition of oxyalkylene is carried out under 0.01-10 bar pressure and 50-200 ℃ of temperature usually, preferred 90-150 ℃.
This reaction is carried out with continuous or intermittent mode.After reacting completely, from reaction mixture, remove unreacted monomer and volatile compound, undertaken by distillation usually.When using dmc catalyst, catalyzer can mainly be retained in the Aethoxy Sklerol, but also can remove, for example by with the oxidizer treatment Aethoxy Sklerol and isolate insoluble compound.
As mentioned above, the Aethoxy Sklerol that is made by the inventive method can be advantageously used in production urethane, especially for producing flexible polyurethane foams.Make Aethoxy Sklerol of the present invention reaction produce urethane according to known method, if desired, Aethoxy Sklerol can be being that the form of mixtures of polyisocyanates is used with having at least two energy other compound with the hydrogen atom of isocyanic ester radical reaction.This reaction is preferably carried out in the presence of traditional catalyst, whipping agent and auxiliary agent and additive.The Aethoxy Sklerol that is made by the inventive method can use separately or to use with the form of mixtures of other H-functional compound.
Polyisocyanates used herein is all isocyanic ester that have two or more isocyanate group in molecule, can use aliphatic isocyanate, for example 1, hexamethylene-diisocyanate (HDI) or isophorone diisocyanate (IPDI), or preferred aromatic isocyanate, for example tolylene diisocyanate (TDI), diphenylmethanediisocyanate (MDI) or, the mixture of diphenylmethanediisocyanate and polymethylene polyphenylene(poly)isocyanate (thick MDI).Can also use and come the isocyanic ester of modification, be called modified isocyanate by introducing carbamate, Uretdion-, isocyanuric acid ester, allophanate, Uretonimine-and other group.
As mixing the compound that uses and have at least two isocyanate reactive groups with Aethoxy Sklerol of the present invention, can use amine, mercaptan, and preferred polyol.In polyvalent alcohol, polyether glycol and polyester polyol have most important industrial significance.The polyether glycol that is used to the to produce urethane base catalysis by oxyalkylene, particularly oxyethane and/or propylene oxide usually adds on the H-functional initiator material and prepares.Polyester polyol prepares by polyfunctional carboxylic acids and polyfunctional alcohol's esterification usually.
The compound that contains at least two energy and the group of isocyanic ester radical reaction also comprises chainextender and/or spendable when needed linking agent.They are that molecular weight is bifunctional amine and/or the alcohol of 60-400 at least.
As whipping agent, make water usually and/or the raw material that is used to produce urethane is the inert compound, they are gasiform under the temperature of urethane reaction, are called the physical action whipping agent, with and composition thereof.Used physical action whipping agent is the hydrocarbon with 2-6 carbon atom, the halon with 2-6 carbon atom, ketone, acetal, ether and rare gas element, for example carbonic acid gas and/or rare gas.
Used catalyzer is amine compound and/or metallic compound, particularly heavy metallic salt and/or organometallic compound particularly.Tertiary amine and/or organometallic compound are particularly useful as catalyzer.
The example of operable auxiliary agent and/or additive is releasing agent, fire retardant, tinting material, filler and/or strongthener.
Usually all raw materials except that polyisocyanates are mixed the formation polyol component industrial, and make itself and polyisocyanates reaction obtain urethane.
Urethane can be by single stage method or by prepolymer method production.Flexible polyurethane foams can be offset plate foam materials or molded foams.
At Kunststoffhandbuch, the 7th volume " urethane ", (Munich Vienna), can find in the 1st edition 1966, the 2 editions 1983 and the 3rd editions 1993 to be used to produce the raw material of urethane and the summary of method Carl-Hanser-Verlag.
Aethoxy Sklerol of the present invention has very narrow molecular weight distribution, and haze-free astoundingly.Because the speed of reaction in the molecule addition of carrying out oxyalkylene by dmc catalyst is very high, so oxyalkylene controllably can be added on the initiator material.Dynamic approach can reduce the block sum that needs the change oxyalkylene or need to change the oxyalkylene ratio of block end in traditional random method subsequently.Have superiority between this makes in the preparation, this is because between block, metering is interrupted in the variation of the oxyalkylene that is metered into and the steady stage necessitates.
The present invention illustrates by following examples.
Embodiment 1
(K2431, Bayer) regeneration twice washes with water then, is neutral until effluent to make 1000 milliliters of strong acid ion-exchangers with 450 gram HCl (37%HCl content).Then with 80.8 gram K
3[Co (CN)
6] solution in 250 ml waters introduces in the ion exchange column.This post of wash-out is neutral once more until effluent then.The Co of gained in effluent: the K ratio was greater than 10: 1.1269 gram effluents are heated to 40 ℃, under agitation mix then with the solution of 80.0 gram zinc acetate (II) dihydrates in 240 gram water.Then the 276.4 gram trimethyl carbinols are added in the suspension, with this suspension in 40 ℃ of restir 30 minutes.Suction filtration goes out solid then, and with 300 milliliters of trimethyl carbinol wash filtrates.Handle the solid obtain thus in drying at room temperature.
Embodiment 2
With 400 gram K
3[Co (CN)
6] solution in 1300 ml waters introduce contain 5000 milliliters of new regenerated strong acid ion-exchangers (K2431, Bayer) in.This post of wash-out is neutral once more until effluent then.The Co of gained in effluent: the K ratio was greater than 10: 1.5000 gram effluents are heated to 40 ℃, and then under agitation (the screw rod agitator 500rpm) mixes with the solution of 396 gram zinc acetate (II) dihydrates in 1400 gram water.Then the 1400 gram trimethyl carbinols are added in the suspension, with this suspension in 40 ℃ of restir 30 minutes.Suction filtration goes out solid then, then with 4000 milliliters of trimethyl carbinol slurryization and filtration once more.It is dry under 50 ℃ and 25 millibars to handle the solid that obtains thus.
Embodiment 3
Strong acid ion-exchanger (Amberlite 252 Na, Rohm ﹠amp with 7 liters of na forms; Haas) place ion exchange column (long: 1 meter, volume: 7.7 liters).Then by make 10% strength hydrochloric acid with 2 bed volume/hour data rate stream crossed ion exchange column 9 hours, make ion-exchanger change into the H form, the sodium content in effusive acid is less than 1ppm.Wash ion-exchanger then with water until neutrality.
The regenerated ion-exchanger is used to prepare the six cyano group cobalt acid that are substantially free of alkali then.For this reason, with 0.24 molar solution of six cyano group cobalts acid potassium with 1 bed volume/hour data rate stream cross ion-exchanger.After reaching 2.5 bed volume, water replaces six cyano group cobalts acid potassium solution.The average six cyano group cobalt acid contents of 2.5 bed volume of gained are 4.5 weight %, and alkali metal content is less than 1ppm.
Below used six cyano group cobalt acid solutions dilute with water suitably.
2432.9 restrain six cyano group cobalt aqueous acids (cobalt contents: 6 grams per liters) be heated to 40 ℃, stir (paddle stirrer simultaneously, 500rpm), add 120 milliliters of tensio-active agent Pluronic PE6100 (BASF AG, the segmented copolymer of propylene oxide and oxyethane) and dissolving.Add the solution of 108.8 gram zinc acetate (II) dihydrates in 400 gram water then, stir simultaneously (paddle stirrer, 500rpm).Then the 400 gram trimethyl carbinols are added in the suspension, in 40 ℃ of restir 30 minutes, suction filtration went out solid then with this suspension.With Ultraturrax wet cake (330 gram) was disperseed 5 minutes in 2000 ml waters.
Embodiment 4:(contrast)
In clean and 1 liter of agitated autoclave of exsiccant, synthesize.With molecular weight is that 80 gram propoxylated glycerols of 400 gram/moles add in the autoclaves, and derives from the catalyst mix of embodiment 3 with 250ppm.Make reactor content be in inert condition with nitrogen, in 125 ℃ of vacuum-treat 1 hour.In 115 ℃, 820 of 68 weight % propylene oxide and 32 weight % oxyethane are restrained mixtures in 1 hour, be metered into.With reaction mixture restir 15 minutes, and in 105 ℃ and 8 millibars of degassings down.Product is handled after filtration.Polyvalent alcohol is muddy.
Hydroxyl value: 33.9mg KOH/g;
Viscosity under 25 ℃: 4966mPas;
Proportion of primary OH groups: 23%;
Mw:15990 gram/mole
D:2.98 (polydispersity, the ratio of Mw and Mn)
Embodiment 5:(contrast)
In clean and 1 liter of agitated autoclave of exsiccant, synthesize.With molecular weight is that 80 gram propoxylated glycerols of 400 gram/moles add in the autoclaves, and derives from the catalyst mix of embodiment 3 with 250ppm.Make reactor content be in inert condition with nitrogen, in 125 ℃ of vacuum-treat 1 hour.In 115 ℃, in 45 minutes, be metered into 560 gram propylene oxide, in 45 minutes, be metered into 260 gram oxyethane then.With reaction mixture restir 15 minutes, and in 105 ℃ and 10 millibars of degassings down.Product is handled after filtration.Polyvalent alcohol is white and heavy-gravity.
Hydroxyl value: 37.4mg KOH/g;
Viscosity under 25 ℃: 1482mPas;
Proportion of primary OH groups: 27%;
Mw: because sample is insoluble, thus can't measure,
Embodiment 6:
In clean and 10 liters of agitated autoclave of exsiccant, synthesize.With molecular weight is that 424.8 gram propoxylated glycerols of 400 gram/moles add in the autoclaves, and derives from the catalyst mix of embodiment 3 with 1.505 grams (based on the 250ppm of solid content).Make reactor content be in inert condition with nitrogen, in 110 ℃ of vacuum-treat 1.5 hours.In 125 ℃, inject 3.5 crust nitrogen, in 3 hours, be metered into 3853.5 gram propylene oxide and 571.1 gram oxyethane altogether then.The ethylene oxide content of this mixture remains 12.8%, and until being metered into 87.5% of oxyalkylene total amount, linearity is reduced to 0% then.Product is handled after filtration.Polyvalent alcohol is transparent.
Hydroxyl value: 35.0mg KOH/g;
Viscosity under 25 ℃: 845mPas;
Proportion of primary OH groups: 5.3%;
Mw:4107 gram/mole
D：1.13
Embodiment 7:
In clean and 10 liters of agitated autoclave of exsiccant, synthesize.With molecular weight is that 423.4 gram propoxylated glycerols of 400 gram/moles add in the autoclaves, and derives from the catalyst mix of embodiment 2 with 1.50 grams (based on the 312ppm of solid content).Make reactor content be in inert condition with nitrogen, in 110 ℃ of vacuum-treat 1.5 hours.In 125 ℃, inject 3.5 crust nitrogen, in 3 hours, be metered into 3819.2 gram propylene oxide altogether then, in 2 hours 43 minutes 52 seconds, be metered into 566.0 gram oxyethane subsequently.The metering rate of propylene oxide is increased continuously, be increased to 1465.1 Grams Per Hours from 0 Grams Per Hour linearity in 60 minutes, kept 1 hour 7 minutes 52 seconds, continuing then increases, and is increased to 1759 Grams Per Hours 36 minutes internal linear, keeps 16 minutes and 8 seconds.When beginning to add propylene oxide, the metering rate that made oxyethane in 60 minutes is increased to 293.2 Grams Per Hours from 0, kept 1 hour 7 minutes 52 seconds, then in 36 minutes continuously linearity be reduced to 0 Grams Per Hour.Original pressure is 3576 millibars, and resulting pressure is 7067 millibars.With this mixture restir 25 minutes, then in 105 ℃ and the 6 millibars degassing 20 minutes down.Product is handled after filtration.Polyvalent alcohol is transparent.
Hydroxyl value: 35.1mg KOH/g;
Viscosity under 25 ℃: 817mPas;
Proportion of primary OH groups: 4.3%;
Mw:4111 gram/mole
D：1.1
Embodiment 8:(contrast)
In clean and 1 liter of agitated autoclave of exsiccant, synthesize.With molecular weight is that 80 gram propoxylated glycerols of 400 gram/moles add in the autoclaves, and derives from the catalyst mix of embodiment 3 with 250ppm.Make reactor content be in inert condition with nitrogen, in 125 ℃ of vacuum-treat 1 hour.In 115 ℃, be metered into 650 gram propylene oxide earlier, be metered into 118 gram oxyethane then, be metered into 98 gram propylene oxide again.With reaction mixture restir 15 minutes, and in 105 ℃ and 6 millibars of degassings down.Product is handled after filtration.Polyvalent alcohol is muddy and highly viscous, so that can not detect viscosity down at 25 ℃.
Hydroxyl value: 35.4mg KOH/g;
Viscosity under 75 ℃: 95.8mPas;
Proportion of primary OH groups: 7%;
D：1.24
Embodiment 9:(contrast)
In clean and 1 liter of agitated autoclave of exsiccant, synthesize.With molecular weight is that 80 gram propoxylated glycerols of 400 gram/moles add in the autoclaves, and derives from the catalyst mix of embodiment 3 with 250ppm.Make reactor content be in inert condition with nitrogen, in 125 ℃ of vacuum-treat 1 hour.In 115 ℃, be metered into the mixture of 651 gram propylene oxide and 118 gram oxyethane earlier, be metered into 98 gram propylene oxide again.With reaction mixture restir 15 minutes, and in 105 ℃ and 6 millibars of degassings down.Product is handled after filtration.Polyvalent alcohol is muddy.
Hydroxyl value: 36.2mg KOH/g;
Viscosity under 25 ℃: 719mPas;
Proportion of primary OH groups: 6%;
D：1.23
Embodiment 10
In clean and 10 liters of agitated autoclave of exsiccant, synthesize.With molecular weight is that 424.8 gram propoxylated glycerols of 400 gram/moles add in the autoclaves, and derives from the catalyst mix of embodiment 2 with 1.505 grams (based on the 312ppm of solid content).Make reactor content be in inert condition with nitrogen, in 110 ℃ of vacuum-treat 1 hour.In 125 ℃, inject 3.5 crust nitrogen, in 3 hours, be metered into 3853.5 gram propylene oxide altogether then, and beginning to add propylene oxide after 1 hour, in 2 hours, be metered into 571.1 and restrain oxyethane.The metering rate of propylene oxide is increased continuously, in 60 minutes, be increased to 1759.9 Grams Per Hours, in 2 hours, be reduced to 352.0 Grams Per Hours then from 0 Grams Per Hour linearity.After beginning to add propylene oxide 1 hour, the metering rate of oxyethane was increased to 352.0 Grams Per Hours from 0 linearity in 2 hours.Original pressure is 3525 millibars, and resulting pressure is 7280 millibars.With this reaction mixture restir 30 minutes, subsequently in 105 ℃ and the 10 millibars degassing 35 minutes down.Product is handled after filtration.Polyvalent alcohol is transparent.
Hydroxyl value: 35.8mg KOH/g;
V
25：767mPas；
Proportion of primary OH groups: 46%;
Mw:3890 gram/mole;
D：1.1
Embodiment 11:(contrast)
In clean and 1 liter of agitated autoclave of exsiccant, synthesize.With molecular weight is that 80 gram propoxylated glycerols of 400 gram/moles add in the autoclaves, and derives from the catalyst mix of embodiment 3 with 250ppm.Make reactor content be in inert condition with nitrogen, in 125 ℃ of vacuum-treat 1 hour.In 115 ℃, be metered into 749 gram propylene oxide earlier, be metered into 118 gram oxyethane again.With reaction mixture restir 15 minutes, and in 105 ℃ and 9 millibars of degassings down.Product is handled after filtration.Polyvalent alcohol is muddy.
Hydroxyl value: 34.8mg KOH/g;
Viscosity under 75 ℃: 95.9mPas;
Proportion of primary OH groups: 11%;
D：1.27
Embodiment 12:(contrast)
In clean and 1 liter of agitated autoclave of exsiccant, synthesize.With molecular weight is that 80 gram propoxylated glycerols of 400 gram/moles add in the autoclaves, and derives from the catalyst mix of embodiment 3 with 250ppm.Make reactor content be in inert condition with nitrogen, in 125 ℃ of vacuum-treat 1 hour.In 115 ℃, be metered into the mixture of 749 gram propylene oxide and 118 gram oxyethane.With reaction mixture restir 15 minutes, and in 105 ℃ and 6 millibars of degassings down.Product is handled after filtration.Polyvalent alcohol is muddy.
Hydroxyl value: 35.5mg KOH/g;
Viscosity under 25 ℃: 919mPas;
Proportion of primary OH groups: 10%;
D：1.34
Compose by the H-NMR that transforms the Aethoxy Sklerol that hydroxyl and record handle thus with isocyanic acid tribromo-acetyl base ester and to measure proportion of primary OH groups.In this collection of illustrative plates, the primary hydroxyl of being measured has different peaks with secondary hydroxyl.
Claims (12)
1. one kind by making at least two kinds of oxyalkylene catalysis add to the method for preparing Aethoxy Sklerol on the H-functional initiator material, wherein at least a multimetal cyanide compounds is as catalyzer, and the addition of oxyalkylene on the initiator material comprises introduces at least a oxyalkylene block, in forming this block process, at least two kinds of oxyalkylenes are metered into together, and change the ratio between each oxyalkylene in this mixture in uniting the introducing process, the change of described ratio is linearity or nonlinearities change.
2. according to the process of claim 1 wherein that the oxyalkylene block contains two kinds of oxyalkylenes, wherein during the formation of this oxyalkylene block, in uniting the introducing process, change the ratio between each oxyalkylene in this mixture.
3. according to the method for claim 1 or 2, wherein the oxyalkylene block comprises whole polyether chain, wherein during the formation of this oxyalkylene block, at least two kinds of oxyalkylenes are metered into together, and change the ratio between each oxyalkylene in this mixture in uniting the introducing process.
4. according to the method for claim 1 or 2, wherein the oxyalkylene block is introduced at the head of polyether chain, wherein during the formation of this oxyalkylene block, at least two kinds of oxyalkylenes are metered into together, and change the ratio between each oxyalkylene in this mixture in uniting the introducing process.
5. according to the method for claim 1 or 2, wherein the oxyalkylene block is introduced at the afterbody of polyether chain, wherein during the formation of this oxyalkylene block, at least two kinds of oxyalkylenes are metered into together, and change the ratio between each oxyalkylene in this mixture in uniting the introducing process.
6. according to the method for claim 1 or 2, wherein the oxyalkylene block is introduced at the polyethers middle-of-chain, wherein during the formation of this oxyalkylene block, at least two kinds of oxyalkylenes are metered into together, and change the ratio between each oxyalkylene in this mixture in uniting the introducing process.
7. according to the method for claim 1, at least a block that wherein only is made of oxyalkylene or is made of the mixture of at least two kinds of constant oxyalkylenes of mol ratio is before the forming of oxyalkylene block and/or introduce afterwards, wherein during the formation of this oxyalkylene block, at least two kinds of oxyalkylenes are metered into together, and change the ratio between each oxyalkylene in this mixture in uniting the introducing process.
8. according to the method for claim 1, the oxyalkylene that wherein is used to form the oxyalkylene block is oxyethane and propylene oxide, wherein during the formation of this oxyalkylene block, at least two kinds of oxyalkylenes are metered into together, and change the ratio between each oxyalkylene in this mixture in uniting the introducing process.
9. according to the process of claim 1 wherein that the catalyzer of the molecule addition that is used for oxyalkylene is a multimetal cyanide compounds.
10. Aethoxy Sklerol according to each method preparation among the claim 1-9.
11. the purposes of Aethoxy Sklerol in producing urethane according to claim 10.
12. one kind is reacted the method for producing urethane by polyisocyanates and the compound with at least two energy and hydrogen atom of isocyanic ester radical reaction, wherein according to the Aethoxy Sklerol of claim 10 as having the compound of at least two energy with the hydrogen atom of isocyanic ester radical reaction.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19960148.8 | 1999-12-14 | ||
| DE19960148A DE19960148A1 (en) | 1999-12-14 | 1999-12-14 | Process for the preparation of polyether alcohols |
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| CN1171927C true CN1171927C (en) | 2004-10-20 |
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| CNB008170738A Expired - Lifetime CN1171927C (en) | 1999-12-14 | 2000-12-06 | Method for production of polyether alcohols |
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| US (1) | US6653441B2 (en) |
| EP (1) | EP1240236B1 (en) |
| JP (1) | JP2003517070A (en) |
| KR (1) | KR100661414B1 (en) |
| CN (1) | CN1171927C (en) |
| AT (1) | ATE275163T1 (en) |
| AU (1) | AU2840201A (en) |
| BR (1) | BR0016343B1 (en) |
| CA (1) | CA2394091C (en) |
| CZ (1) | CZ20022018A3 (en) |
| DE (2) | DE19960148A1 (en) |
| ES (1) | ES2225303T3 (en) |
| HU (1) | HUP0203763A2 (en) |
| MX (1) | MXPA02005160A (en) |
| PL (1) | PL207514B1 (en) |
| RU (1) | RU2263684C2 (en) |
| WO (1) | WO2001044347A1 (en) |
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| DE10240186A1 (en) * | 2002-08-28 | 2004-03-11 | Basf Ag | Process for the production of low-emission flexible polyurethane foams |
| US7645717B2 (en) * | 2003-05-22 | 2010-01-12 | Dow Global Technologies, Inc. | Nano-scale DMC catalyst particles |
| DE10324998A1 (en) * | 2003-06-03 | 2004-12-23 | Basf Ag | Production of polyether alcohols using DMC catalysis |
| JP4158858B2 (en) * | 2003-12-04 | 2008-10-01 | 多摩川精機株式会社 | Rotation angle detector |
| DE102004047524A1 (en) * | 2004-09-28 | 2006-03-30 | Basf Ag | Process for the production of flexible polyurethane foams |
| DE102004047406A1 (en) * | 2004-09-28 | 2006-03-30 | Basf Ag | Process for the production of flexible polyurethane foams |
| DE102005034001A1 (en) * | 2005-07-18 | 2007-01-25 | Basf Ag | Process for the preparation of polyether alcohols |
| DE102005041142A1 (en) * | 2005-08-30 | 2007-03-01 | Basf Ag | Production of polyether-alcohol for making polyurethane foam, involves reacting a propoxylated starter in a tubular reactor supplied with alkylene oxide mixtures with increasing proportions of ethylene oxide |
| JP5642558B2 (en) | 2008-01-29 | 2014-12-17 | ビーエーエスエフ ソシエタス・ヨーロピアＢａｓｆ Ｓｅ | Method for producing polyether alcohol |
| EP2090596A1 (en) * | 2008-02-13 | 2009-08-19 | Construction Research and Technology GmbH | Copolymer with polyether side chains and hydroxyalkyl and acid building blocks |
| US7973110B2 (en) * | 2008-06-16 | 2011-07-05 | Construction Research & Technology Gmbh | Copolymer synthesis process |
| CN101684184A (en) | 2008-09-27 | 2010-03-31 | 巴斯夫欧洲公司 | Polyurethane sole obtained by using renewable raw materials |
| CN102498145B (en) | 2009-07-10 | 2013-10-23 | 巴斯夫欧洲公司 | Method for producing polyols on basis of renewable resources |
| JP5886701B2 (en) * | 2011-07-14 | 2016-03-16 | 松本油脂製薬株式会社 | Alkylene oxide adduct and process for producing the same |
| EP2548906A1 (en) * | 2011-07-18 | 2013-01-23 | Bayer MaterialScience AG | Method for activating double metal cyanide catalysts to produce polyether polyols |
| JP6051005B2 (en) * | 2011-10-21 | 2016-12-21 | 松本油脂製薬株式会社 | Method for producing alkylene oxide adduct |
| EP2730602A1 (en) | 2012-11-09 | 2014-05-14 | Bayer MaterialScience AG | Method for manufacturing polyether carbonate polyols |
| KR20150084820A (en) | 2012-11-09 | 2015-07-22 | 바이엘 머티리얼사이언스 아게 | Method for producing polyether carbonate polyols |
| KR102062491B1 (en) * | 2019-06-10 | 2020-01-03 | 박기준 | Manufacturing method of civil engineering building materials using inorganic sludge and soft material |
| GB202003002D0 (en) | 2020-03-02 | 2020-04-15 | Crane Ltd | Method of preparation of a polyol block copolymer |
| GB202003003D0 (en) | 2020-03-02 | 2020-04-15 | Econic Tech Ltd | A polyol block copolymer |
| EP3878885A1 (en) | 2020-03-10 | 2021-09-15 | Covestro Deutschland AG | Process for producing polyether carbonate polyols |
| PL442356A1 (en) * | 2022-09-26 | 2024-04-02 | Pcc Rokita Spółka Akcyjna | Polyether polyol, its production method and its use, and flexible polyurethane foam |
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| DD237178A1 (en) * | 1982-10-14 | 1986-07-02 | Adw Ddr | METHOD FOR PRODUCING POLYURETHANE ELASTOMERS |
| DD275695A1 (en) * | 1987-06-17 | 1990-01-31 | Schwarzheide Synthesewerk Veb | PROCESS FOR PREPARING POLYETHERAL COCOOLS HAVING HIGH AEQUIVALENT WEIGHTS |
| US5677413A (en) | 1995-06-15 | 1997-10-14 | Arco Chemical Technology, L.P. | Polyurethane elastomers exhibiting improved demold green strength and water absorption and haze-free polyols suitable for their preparation |
| US5605939A (en) | 1996-01-26 | 1997-02-25 | Arco Chemical Technology, L.P. | Poly(oxypropylene/oxyethylene) random polyols useful in preparing flexible high resilience foam with reduced tendencies toward shrinkage and foam prepared therewith |
| US6008263A (en) * | 1998-04-03 | 1999-12-28 | Lyondell Chemical Worldwide, Inc. | Molded and slab polyurethane foam prepared from double metal cyanide complex-catalyzed polyoxyalkylene polyols and polyols suitable for the preparation thereof |
| US6066683A (en) * | 1998-04-03 | 2000-05-23 | Lyondell Chemical Worldwide, Inc. | Molded and slab polyurethane foam prepared from double metal cyanide complex-catalyzed polyoxyalkylene polyols and polyols suitable for the preparation thereof |
| JP2000044505A (en) * | 1998-07-30 | 2000-02-15 | Asahi Denka Kogyo Kk | Polyether and its production |
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| Publication number | Publication date |
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| US20020183482A1 (en) | 2002-12-05 |
| CA2394091C (en) | 2007-01-30 |
| PL355884A1 (en) | 2004-05-31 |
| KR100661414B1 (en) | 2006-12-27 |
| EP1240236B1 (en) | 2004-09-01 |
| MXPA02005160A (en) | 2002-12-09 |
| PL207514B1 (en) | 2010-12-31 |
| BR0016343A (en) | 2002-08-27 |
| ATE275163T1 (en) | 2004-09-15 |
| JP2003517070A (en) | 2003-05-20 |
| KR20020063216A (en) | 2002-08-01 |
| DE19960148A1 (en) | 2001-06-21 |
| CZ20022018A3 (en) | 2003-01-15 |
| CN1409736A (en) | 2003-04-09 |
| RU2002119023A (en) | 2004-01-10 |
| ES2225303T3 (en) | 2005-03-16 |
| DE50007641D1 (en) | 2004-10-07 |
| AU2840201A (en) | 2001-06-25 |
| US6653441B2 (en) | 2003-11-25 |
| CA2394091A1 (en) | 2001-06-21 |
| HUP0203763A2 (en) | 2003-04-28 |
| BR0016343B1 (en) | 2011-05-03 |
| RU2263684C2 (en) | 2005-11-10 |
| EP1240236A1 (en) | 2002-09-18 |
| WO2001044347A1 (en) | 2001-06-21 |
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